CN102671617B - A preparation method of a material for adsorbing refractory organic pollutants - Google Patents
A preparation method of a material for adsorbing refractory organic pollutants Download PDFInfo
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Abstract
本发明涉及一种用于吸附难降解有机污染物的材料的制备方法。以纳米铁、镁盐、铝盐、烧碱为无机反应物,以阴离子表面活性剂为功能化剂,将阴离子表面活性剂与纳米铁混合均匀后,加入到烧碱与铝盐的混合溶液中,混匀,再缓慢加入镁盐溶液,混合10~30分钟,静置12小时以上,分离得到蓝色沉淀物,即为用于吸附包括染料或持久性有机物等的难降解有机污染物的材料。将此材料按0.1~1%加入到有机废水中,具有优良的吸附性能和磁分离性能。本发明具有原料易得、工艺简单、成本低廉、产品对染料或憎水性有机物吸附量大、磁分离效果好等优点,可用于有机工业废水的吸附处理。The invention relates to a preparation method of a material for adsorbing refractory organic pollutants. With nano-iron, magnesium salt, aluminum salt and caustic soda as inorganic reactants and anionic surfactant as functional agent, after mixing the anionic surfactant and nano-iron evenly, add it to the mixed solution of caustic soda and aluminum salt, mix Mix well, then slowly add magnesium salt solution, mix for 10-30 minutes, let stand for more than 12 hours, separate and obtain blue precipitate, which is the material used to adsorb refractory organic pollutants including dyes or persistent organic compounds. The material is added into organic waste water by 0.1-1%, and has excellent adsorption performance and magnetic separation performance. The invention has the advantages of easy-to-obtain raw materials, simple process, low cost, large adsorption capacity of dyes or hydrophobic organic matter, good magnetic separation effect, etc., and can be used for adsorption treatment of organic industrial wastewater.
Description
技术领域 technical field
本发明涉及一种用于吸附难降解有机污染物的材料的制备方法,具体是处理有机废水的吸附材料的生产工艺。属于环境污染控制领域。The invention relates to a preparation method of a material for adsorbing refractory organic pollutants, in particular to a production process of an adsorption material for treating organic waste water. It belongs to the field of environmental pollution control.
背景技术 Background technique
染料、医药、农药、化工等生产过程中产生了大量的废水排放到环境中,高浓度有机物,特别是持久性有机污染物给人类和生态环境带来严重灾难。例如,超过10000种的染料已商业化生产,其中使用量的5%-10%排入水环境中。染料分子中大都含有芳香基结构,耐光、耐热、耐氧化,有些染料可引起过敏、皮炎、皮肤红肿,甚至可诱发癌症、基因突变等。因此,在进入自然水体前必须去除废水中有机污染物。有机废水处理方法主要有物理法、化学法、生物法。物理法主要包括:膜分离法、磁分离法及吸附法。膜分离法处理有机和颜色废水始于上世纪70年代初。但膜的价格较高,更换频率较快,处理成本较高。磁分离法是利用元素或组分磁敏感性的差异,借助外磁场将物质进行磁场处理,从而达到强化分离的过程,目前已成为一门新兴的水处理技术。吸附是利用表面具有多孔的一些固体作为吸附剂,当废水与吸附剂接触时,废水中一种或数种污染物被吸附在固体表面从而达到废水净化的目的。在有机废水处理中,吸附法主要用作预处理或生化后的深度处理。吸附法的应用范围比较广泛,没有专一性。吸附剂分为人工和天然吸附剂两种,常用的吸附剂有活性炭、氧化铝、木片、天然粘土、水稻磨粉废料、硅胶、氢氧化物、污泥、微生物活体或死细胞等,但大多吸附平衡时间长,再生后效果明显降低,选择性差,化学需氧量(COD)降低幅度小。活性炭吸附是目前应用最广泛的有机和颜色废水处理方法,但活性炭吸附时间长,再生比较困难。膨润土在我国储量大,价格便宜。人们常用表面活性剂改性膨润土,吸附性能可比原土高出1~2个数量级。用于有机废水处理时,表面修饰容易产生表面活性剂脱附,虽然废水中有机物浓度降低,但COD降低不明显。化学法主要分为混凝沉淀法、氧化法及电化学方法。混凝沉淀技术是对废水进行一级处理的主要步骤。它是利用染料本身的带电特性,将两种或多种带相反电荷的污水混和进行处理,或者利用混凝剂与污水混和进行处理的一种技术。在絮凝沉淀过程中起主要作用的是絮凝剂,但传统的低分子量絮凝剂投放量大,产泥量多。常规的混凝剂在处理一些水溶性,特别是在处理阳离子染料、活性染料废水时,单独采用絮凝剂的脱色效果不理想。氧化法分为化学氧化法和高级氧化法,都是将染料的发色基因氧化破坏而脱色的处理工艺。高级氧化技术包括湿式氧化法、Fenton试剂法以及光催化氧化法等,具有很好的脱色能力,但是成本较高,COD降低效果不好。电化学技术处理废水具有氧化还原、凝聚、杀菌消毒和吸附等多种功能,但是彻底氧化分解水中有机污染物,能耗较高,设备成本也较高。采用微生物法对有机物进行吸附是近几年逐渐发展起来的,该方法具有无废物、利用完全等优点,但脱色周期长,且对于环境有一定的要求。由于有机污染物特别是持久性有机污染物对环境和人体健康造成的危害大,因此设计制备吸附效率高、吸附与分离性能好的新型吸附材料来消除污染具有重要意义。A large amount of waste water is discharged into the environment during the production of dyes, medicines, pesticides, and chemicals. High concentrations of organic matter, especially persistent organic pollutants, have brought serious disasters to humans and the ecological environment. For example, more than 10,000 dyes have been produced commercially, with 5%-10% of the amount used being discharged into the aquatic environment. Most of the dye molecules contain aromatic groups, which are resistant to light, heat, and oxidation. Some dyes can cause allergies, dermatitis, redness and swelling of the skin, and even induce cancer and gene mutations. Therefore, organic pollutants in wastewater must be removed before entering natural water bodies. Organic wastewater treatment methods mainly include physical, chemical and biological methods. Physical methods mainly include: membrane separation method, magnetic separation method and adsorption method. Membrane separation method to treat organic and colored wastewater began in the early 1970s. However, the price of the membrane is higher, the replacement frequency is faster, and the disposal cost is higher. Magnetic separation is a process of using the difference in magnetic susceptibility of elements or components to treat the material with the help of an external magnetic field, so as to achieve enhanced separation. It has become an emerging water treatment technology. Adsorption is the use of some solids with porous surfaces as adsorbents. When the wastewater is in contact with the adsorbent, one or several pollutants in the wastewater are adsorbed on the solid surface to achieve the purpose of wastewater purification. In the treatment of organic wastewater, the adsorption method is mainly used for pretreatment or advanced treatment after biochemical treatment. Adsorption method has a wide range of applications and is not specific. Adsorbents are divided into artificial and natural adsorbents. Commonly used adsorbents include activated carbon, alumina, wood chips, natural clay, rice milling waste, silica gel, hydroxide, sludge, living microorganisms or dead cells, etc., but most of them are The adsorption equilibrium time is long, the effect after regeneration is obviously reduced, the selectivity is poor, and the reduction of chemical oxygen demand (COD) is small. Activated carbon adsorption is currently the most widely used organic and colored wastewater treatment method, but activated carbon adsorption takes a long time and regeneration is difficult. Bentonite has a large reserve in my country and is cheap. People often use surfactants to modify bentonite, and the adsorption performance can be 1 to 2 orders of magnitude higher than that of the original soil. When used in organic wastewater treatment, surface modification is prone to desorption of surfactants. Although the concentration of organic matter in wastewater is reduced, the reduction of COD is not obvious. Chemical methods are mainly divided into coagulation precipitation method, oxidation method and electrochemical method. Coagulation and sedimentation technology is the main step in the primary treatment of wastewater. It is a technology that uses the charging characteristics of the dye itself to mix two or more oppositely charged sewage, or uses a coagulant to mix sewage. The flocculant plays a major role in the flocculation and sedimentation process, but the traditional low molecular weight flocculant has a large dosage and produces a large amount of sludge. Conventional coagulants are used in the treatment of some water-soluble, especially in the treatment of cationic dyes and reactive dye wastewater, the decolorization effect of flocculants alone is not ideal. Oxidation methods are divided into chemical oxidation methods and advanced oxidation methods, both of which are treatment processes that oxidize and destroy the color-forming genes of dyes and decolorize them. Advanced oxidation technology includes wet oxidation method, Fenton reagent method and photocatalytic oxidation method, etc., which have good decolorization ability, but the cost is high, and the COD reduction effect is not good. Electrochemical technology to treat wastewater has multiple functions such as redox, coagulation, sterilization, and adsorption. However, the complete oxidation and decomposition of organic pollutants in water requires high energy consumption and high equipment costs. The use of microbial methods to adsorb organic matter has been gradually developed in recent years. This method has the advantages of no waste and complete utilization, but the decolorization cycle is long and has certain requirements for the environment. Because organic pollutants, especially persistent organic pollutants, are harmful to the environment and human health, it is of great significance to design and prepare new adsorption materials with high adsorption efficiency and good adsorption and separation performance to eliminate pollution.
发明内容 Contents of the invention
本发明的目的在于公开一种用于典型有机污染物吸附的材料制备方法。用本发明方法得到难降解有机污染物(染料、持久性有机污染物等)的吸附材料,用于有机废水的吸附处理,而且吸附容量大、易分离和可再循环利用。The purpose of the present invention is to disclose a material preparation method for adsorption of typical organic pollutants. The adsorption material of refractory organic pollutants (dyes, persistent organic pollutants, etc.) obtained by the method of the invention is used for adsorption treatment of organic waste water, and has large adsorption capacity, easy separation and recyclable utilization.
为了实现上述目的,本发明选用镁盐、铝盐、纳米铁、烧碱为无机原料,其中镁盐原料包括氯化镁和硝酸镁,铝盐原料包括硫酸铝和硝酸铝,阴离子表面活性剂包括多烷基苯磺酸钠或多烷基硫酸钠。将阴离子表面活性剂与纳米铁混合均匀后,加入铝盐与纯碱的混合溶液中,混匀后,再与镁盐溶液混合反应,分离沉淀物即为用于难降解有机污染物(染料、持久性有机污染物等)的吸附材料。In order to achieve the above object, the present invention selects magnesium salt, aluminum salt, nano-iron, and caustic soda as inorganic raw materials, wherein the magnesium salt raw material includes magnesium chloride and magnesium nitrate, the aluminum salt raw material includes aluminum sulfate and aluminum nitrate, and the anionic surfactant includes polyalkylene Sodium benzenesulfonate or sodium polyalkylsulfate. After mixing the anionic surfactant and nano-iron evenly, add it to the mixed solution of aluminum salt and soda ash. Adsorbent materials for organic pollutants, etc.
具体工艺如下:The specific process is as follows:
第一步,原料的选择和配制The first step, the selection and preparation of raw materials
将市售的工业级氯化镁或硝酸镁加水,配制成重量百分比浓度为10~30%的溶液A;Add water to commercially available industrial grade magnesium chloride or magnesium nitrate to prepare a solution A with a concentration of 10% to 30% by weight;
将市售的工业级硝酸铝或硫酸铝加水配制成重量百分比浓度为5~30%的溶液B;Commercially available industrial-grade aluminum nitrate or aluminum sulfate is added with water to prepare a solution B with a concentration of 5% to 30% by weight;
将市售的工业级阴离子表面活性剂中加水配制成重量百分浓度为1~2%的溶液C;Add water to a commercially available industrial grade anionic surfactant to prepare a solution C with a concentration of 1 to 2% by weight;
选择市售的纳米铁为原料,在纳米铁中加水配制成重量百分浓度为1~5%溶液D;Selecting commercially available nano-iron as raw material, adding water to the nano-iron to prepare a solution D with a concentration of 1 to 5% by weight;
将市售的工业级烧碱加水制成重量百分浓度为5~20%溶液E。Commercially available industrial grade caustic soda is added with water to make solution E with a concentration of 5-20% by weight.
上述阴离子表面活性剂为十二烷基磺酸钠,或十四烷基磺酸钠,或十六烷基磺酸钠,或十八烷基磺酸钠,或十二烷基苯磺酸钠。The above-mentioned anionic surfactant is sodium dodecylsulfonate, or sodium tetradecylsulfonate, or sodium hexadecylsulfonate, or sodium octadecylsulfonate, or sodium dodecylbenzenesulfonate .
上述纳米铁为市售的粒径20nm的铁粉;The above-mentioned nano-iron is commercially available iron powder with a particle diameter of 20nm;
第二步,材料的制备The second step, the preparation of materials
首先,按重量份数等量量取上述A、B、C、D、E溶液,将溶液C与溶液D混合10~30分钟得到一种液体,再将溶液B与溶液E混合,搅拌溶解得到另一种液体,然后将两种液体混合、搅拌下,再将溶液A缓慢加入其中,搅拌反应10~30分钟得到反应液,将反应液静置陈化12~24小时,最后,在反应器底部放置磁铁块,2小时后弃去澄清液,反应器的底部留下的蓝色沉淀物,即为用于吸附难降解有机污染物的材料;First, take the above-mentioned A, B, C, D, E solutions in equal parts by weight, mix solution C and solution D for 10 to 30 minutes to obtain a liquid, then mix solution B and solution E, stir and dissolve to obtain Another liquid, then mix the two liquids and stir, then slowly add solution A to it, stir and react for 10-30 minutes to obtain a reaction liquid, leave the reaction liquid to stand for 12-24 hours, and finally, in the reactor Place a magnet block at the bottom, discard the clarified solution after 2 hours, and the blue precipitate left at the bottom of the reactor is the material used to adsorb refractory organic pollutants;
第三步,材料的保存或使用Step 3, Preservation or Use of Materials
将该吸附难降解有机污染物的材料加水,配制成重量百分比为3~10%液体产品,直接用于吸附难降解有机污染物;adding water to the material for adsorbing refractory organic pollutants to prepare a liquid product with a weight percentage of 3-10%, which is directly used for adsorbing refractory organic pollutants;
或将该吸附难降解有机污染物的材料烘干、粉碎,制得便于保存和运输的粉体产品。Or dry and pulverize the material that adsorbs refractory organic pollutants to obtain a powder product that is convenient for storage and transportation.
上述在反应器底部放置磁铁块,是按照3000ml反应液使用市售的直径20厘米、厚2厘米的圆盘磁铁,磁铁块由上海金昆磁电科技有限公司提供。The above-mentioned placement of the magnet block at the bottom of the reactor is to use a commercially available disc magnet with a diameter of 20 cm and a thickness of 2 cm according to the 3000ml reaction solution. The magnet block is provided by Shanghai Jinkun Magnetic Technology Co., Ltd.
上述第三步直接用于吸附难降解有机污染物是,向色度为1~10万度染料废水或浓度10~5000mg/l有机物废水中加入制备得到的浓度为重量百分比3~10%的液体材料,液体材料投加量为废水体积的2~20%体积百分比,搅拌5~30分钟,在废水底部放置直径10~20厘米、厚度为1~2厘米的磁铁10~30分钟,吸附沉淀物为富集了有机污染物的残渣,残渣经高温焙烧,分解所吸附的有机物质,得到可循环利用的磁性无机材料。The above-mentioned third step is directly used to adsorb refractory organic pollutants, adding the prepared liquid with a concentration of 3 to 10% by weight to the dye wastewater with a chroma of 10,000 to 100,000 degrees or organic waste with a concentration of 10 to 5,000 mg/l. Material, liquid material dosage is 2-20% volume percentage of the waste water volume, stir for 5-30 minutes, place a magnet with a diameter of 10-20 cm and a thickness of 1-2 cm at the bottom of the waste water for 10-30 minutes to absorb the sediment In order to enrich the residues of organic pollutants, the residues are roasted at high temperature to decompose the adsorbed organic substances to obtain recyclable magnetic inorganic materials.
本发明的优点如下:The advantages of the present invention are as follows:
1.本发明具有工艺简单,原料易得、价格便宜等优点。1. The present invention has the advantages of simple process, readily available raw materials, and low price.
2.本发明得到的产品对难降解有机污染物具有良好的吸附性能,包括碱性染料、阳离子染料、分散染料、有机胺、有机氯和有机磷杀虫剂、杀菌剂、表面活性剂、染发剂、内分泌干扰素、抗生素等,吸附率60~100%。2. The product obtained by the present invention has good adsorption properties to refractory organic pollutants, including basic dyes, cationic dyes, disperse dyes, organic amines, organochlorine and organophosphorus insecticides, bactericides, surfactants, hair dyes Drugs, endocrine disruptors, antibiotics, etc., the adsorption rate is 60-100%.
3.与传统吸附剂相比,本发明得到的材料可以直接分散到废水中吸附有机污染物,然后通过磁铁分离,不需使用过滤、离心等手段,具有效果好、速度快、省时省电等优点,在有机废水处理中有较大应用潜力。3. Compared with traditional adsorbents, the materials obtained in the present invention can be directly dispersed into wastewater to absorb organic pollutants, and then separated by magnets without using filtration, centrifugation and other means, with good effect, fast speed, time-saving and power-saving And other advantages, it has great application potential in organic wastewater treatment.
4.使用后的残渣可经高温焙烧,分解所吸附的有机物,制备可用于吸附重金属的磁性吸附剂。4. The residue after use can be roasted at high temperature to decompose the adsorbed organic matter and prepare a magnetic adsorbent that can be used to adsorb heavy metals.
具体实施方式 Detailed ways
实施例1Example 1
第一步,原料的选择和配制The first step, the selection and preparation of raw materials
选用市售的工业级氯化镁或硝酸镁,将水加入其中,配制成重量百分比浓度为10%的溶液,简称为溶液A;Select commercially available industrial-grade magnesium chloride or magnesium nitrate, add water to it, and prepare a solution with a concentration of 10% by weight, which is referred to as solution A;
选用市售的工业级硝酸铝或硫酸铝,将水加入其中,配制成重量百分比浓度为20%的溶液,简称为溶液B;Select commercially available industrial-grade aluminum nitrate or aluminum sulfate, add water to it, and prepare a solution with a concentration of 20% by weight, which is referred to as solution B;
选用市售的工业级十二烷基苯磺酸钠,将水加入其中,配制成重量百分浓度为1%的溶液,简称为溶液C;Select commercially available industrial-grade sodium dodecylbenzenesulfonate, add water to it, and prepare a solution with a concentration of 1% by weight, which is referred to as solution C;
选择市售的纳米铁为原料,纳米铁为粒径20nm的铁粉,在纳米铁中加水,配制成重量百分浓度为1%溶液,简称为溶液D;Select commercially available nano-iron as raw material, the nano-iron is iron powder with a particle size of 20nm, add water to the nano-iron to prepare a solution with a concentration of 1% by weight, referred to as solution D;
将市售的工业级烧碱加水,制成重量百分浓度为5%溶液,简称为溶液E。Add water to commercially available industrial grade caustic soda to make a solution with a concentration of 5% by weight, which is called solution E for short.
第二步,材料的制备The second step, the preparation of materials
首先,按重量份数等量量取上述A、B、C、D、E溶液各500ml,将溶液C与溶液D混合20分钟,再将溶液B与溶液E混合,搅拌溶解,然后将两液体混合、搅拌,再将溶液A缓慢加入其中,搅拌反应20分钟,将反应液静置陈化12小时,最后,在反应器底部放置磁铁块,2小时后弃去澄清液,反应器的底部留下的蓝色沉淀物,即为吸附难降解有机污染物的材料;First, take 500ml of each of the above-mentioned solutions A, B, C, D, and E in equal parts by weight, mix solution C and solution D for 20 minutes, then mix solution B and solution E, stir to dissolve, and then mix the two liquids Mix and stir, then slowly add solution A to it, stir and react for 20 minutes, leave the reaction solution to stand and age for 12 hours, and finally, place a magnet block at the bottom of the reactor, discard the clear solution after 2 hours, and leave the solution at the bottom of the reactor The blue precipitate below is the material for adsorbing refractory organic pollutants;
将蓝色沉淀物配制成重量百分比为5%材料的液体,直接用于吸附难降解有机污染物。The blue precipitate is formulated into a liquid with a weight percentage of 5% material, which is directly used to adsorb refractory organic pollutants.
实施例2Example 2
染料废水吸附处理:取1000ml某合成染料厂甲基蓝废水于烧杯中,加入实施例1制备得到的外观为蓝色、含量为5%的液体材料100ml,搅拌20分钟后,在烧杯下方贴底放置直径为20cm磁铁块,静置30分钟。检测结果表明:原废水中色度为24500度,吸附处理后澄清液中色度30度,去除率99.9%。因此,该材料对染料废水有优良的处理效果。Adsorption treatment of dye wastewater: Take 1000ml of methylene blue wastewater from a synthetic dye factory in a beaker, add 100ml of the liquid material with a blue appearance and a content of 5% prepared in Example 1, stir for 20 minutes, and stick to the bottom of the beaker Place a magnet block with a diameter of 20 cm and let it stand for 30 minutes. The test results show that the chroma in the raw wastewater is 24500 degrees, the chroma in the clarified liquid after adsorption treatment is 30 degrees, and the removal rate is 99.9%. Therefore, the material has an excellent treatment effect on dye wastewater.
残渣经500度下焙烧2小时,分解所吸附的有机物,粉碎成粉末后仍可被磁铁吸附,可作为重金属的磁性吸附剂继续使用。The residue is calcined at 500 degrees for 2 hours to decompose the adsorbed organic matter, and it can still be adsorbed by a magnet after being pulverized into powder, and can be used as a magnetic adsorbent for heavy metals.
实施例3Example 3
农药废水吸附处理:取1000ml某农药厂辛硫磷废水于烧杯中,加入实施例1制备得到的外观为蓝色、含量为5%的液体材料60ml,搅拌20分钟后,在烧杯下方贴底放置直径为20cm磁铁块,静置20分钟。检测结果表明:原废水中辛硫磷浓度为120mg/l,吸附处理后澄清液中辛硫磷浓度为15mg/l,去除率87.5%。因此,该材料对憎水性有机物废水有良好的处理效果。Adsorption treatment of pesticide wastewater: Take 1000ml of phoxim wastewater from a pesticide factory in a beaker, add 60ml of the liquid material with a blue appearance and a content of 5% prepared in Example 1, stir for 20 minutes, and place it on the bottom of the beaker A magnet block with a diameter of 20 cm was left to stand for 20 minutes. The test results show that the concentration of phoxim in the raw wastewater is 120mg/l, and the concentration of phoxim in the clarified liquid after adsorption treatment is 15mg/l, with a removal rate of 87.5%. Therefore, the material has a good treatment effect on hydrophobic organic waste water.
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